CN111408176A - Method and device for purifying multidimensional nano material - Google Patents
Method and device for purifying multidimensional nano material Download PDFInfo
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- CN111408176A CN111408176A CN202010153071.0A CN202010153071A CN111408176A CN 111408176 A CN111408176 A CN 111408176A CN 202010153071 A CN202010153071 A CN 202010153071A CN 111408176 A CN111408176 A CN 111408176A
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- 239000002086 nanomaterial Substances 0.000 title claims abstract description 43
- 238000000034 method Methods 0.000 title claims abstract description 25
- 238000003756 stirring Methods 0.000 claims abstract description 54
- 239000000243 solution Substances 0.000 claims abstract description 34
- 239000012528 membrane Substances 0.000 claims abstract description 21
- 238000002347 injection Methods 0.000 claims abstract description 16
- 239000007924 injection Substances 0.000 claims abstract description 16
- 238000000746 purification Methods 0.000 claims abstract description 14
- 239000000706 filtrate Substances 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims description 43
- 239000002904 solvent Substances 0.000 claims description 30
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 19
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 18
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 12
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 12
- 239000012452 mother liquor Substances 0.000 claims description 11
- 239000006227 byproduct Substances 0.000 claims description 10
- 238000002386 leaching Methods 0.000 claims description 10
- 238000007865 diluting Methods 0.000 claims description 7
- 239000003208 petroleum Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000003085 diluting agent Substances 0.000 claims description 5
- 239000012141 concentrate Substances 0.000 claims description 2
- 239000011148 porous material Substances 0.000 claims description 2
- 238000013019 agitation Methods 0.000 claims 3
- 239000002135 nanosheet Substances 0.000 abstract description 11
- 239000002070 nanowire Substances 0.000 abstract description 5
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 10
- 239000002585 base Substances 0.000 description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000002042 Silver nanowire Substances 0.000 description 5
- 239000002105 nanoparticle Substances 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 229910052582 BN Inorganic materials 0.000 description 4
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000005530 etching Methods 0.000 description 3
- 229910052709 silver Inorganic materials 0.000 description 3
- 239000004332 silver Substances 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 238000000498 ball milling Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
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- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 1
- 238000000149 argon plasma sintering Methods 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
- B01D29/13—Supported filter elements
- B01D29/23—Supported filter elements arranged for outward flow filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/60—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
- B01D29/606—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration by pressure measuring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/76—Handling the filter cake in the filter for purposes other than for regenerating
- B01D29/78—Handling the filter cake in the filter for purposes other than for regenerating for washing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/76—Handling the filter cake in the filter for purposes other than for regenerating
- B01D29/86—Retarding cake deposition on the filter during the filtration period, e.g. using stirrers
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention provides a method and a device for purifying multidimensional nano materials, wherein the device comprises a filter cylinder, a stirring device, a solution injection system and a filtrate outflow and collection system, the filter cylinder consists of a filter base, a filter framework and a filter membrane attached to the filter framework, and the filter membrane is fixed on the filter cylinder through the framework on the filter cylinder and is vertical to the filter base; the purification method has the advantages of simple steps, mild conditions, high efficiency and high speed, and can be applied to the purification of the nano wires and the nano sheets.
Description
Technical Field
The invention relates to the field of preparation of multidimensional nano metal powder and packaging and interconnection of semiconductor chips, in particular to a method and a device for preparing a pure multidimensional nano material.
Background
The chemical preparation and synthesis of the nano material are mainly divided into a top-down method and a bottom-up method, wherein the top-down method comprises the following steps: the nano structure required by people is prepared by a substance with larger size (from micron level to centimeter level) through various etching technologies, and the nano structure has the advantages that various exotic three-dimensional structures can be conveniently prepared; the 'from bottom to top' is that some small structural units (such as atoms, molecules, nano particles and the like) are self-assembled through weak interaction to form a relatively large and complex structural system on the nano scale, and the structural system has the advantages of saving materials, controlling the appearance, controlling the thickness of the materials and the like and has the defect of difficult synthesis. However, the production of the multi-dimensional nano material from top to bottom or from bottom to top is accompanied by the production of byproducts. For example, taking the preparation of silver nanowires as an example, the formation of nanoparticles and nanoprobes as byproducts is inevitable during the preparation of silver nanowires because the formation of crystal nuclei is not instantaneous, and when the oriented growth of silver atoms on the surface of the crystal nuclei is limited, the crystal nuclei grow along multiple paths and thus the formation of byproducts is caused. In addition, some surfactants such as PVP and metal salts are also present in the reaction product, which can greatly degrade the performance of the materials in the device if used directly without purification treatment. Taking the transparent conductive network of the silver nanowires as an example, the existence of PVP can obviously improve the contact resistance between the nanowires and the square resistance of the conductive network, thereby reducing the electrical property of the nanowires; the nanoparticles cannot provide effective conductive paths, so that the improvement of the electrical properties is very limited, and the existence of the nanoparticles can cause light scattering in a visible light range to reduce the optical properties of the transparent conductive film. The two-dimensional material takes boron nitride nanosheets as an example, and at present, common literature reports that hexagonal boron nitride is generally prepared by mechanical ball milling or alkali etching on the boron nitride nanosheets, but a large amount of boron nitride nanoparticle byproducts are generated in the mechanical ball milling or etching process, so that the separation of particles and the nanosheets becomes a difficult point.
At present, the post-treatment purification of the multi-dimensional nano material comprises methods such as centrifugation, filtration, selective sedimentation, electrophoresis, dialysis and the like, but all the methods have limitations, mainly comprising complex and complicated steps, low efficiency and long time consumption, and are not beneficial to large-scale and repeatable preparation in the actual production process. Therefore, in order to further improve the quality of multi-dimensional nanomaterials and reduce production costs for commercial applications, it is necessary to develop an industrially scalable, high-performance, cost-controllable process for large-scale purification of multi-dimensional nanomaterials.
Disclosure of Invention
Aiming at the technical problems in the prior art, the invention provides a device for purifying multidimensional nanomaterials, which comprises a filter cylinder, a stirring device, a solution injection system and a filtrate outflow and collection system, wherein the filter cylinder consists of a filter base, a filter framework and a filter membrane attached to the filter framework, and the filter membrane is fixed on the filter base through the filter framework and is vertical to the filter base.
Preferably, the size of the filter pores of the filter membrane is 100 nm-10 μm.
Preferably, the stirring device comprises a stirring paddle connected to an electric motor.
Preferably, the stirring paddle is selected from one of a single screw propeller, a double screw propeller and a porous stirring paddle.
Preferably, the electric motor is connected with a stirring paddle, and stirring is carried out to generate centrifugal force in purification so as to provide filtering pressure for the nano material to filter out byproducts.
Preferably, the solution injection system is responsible for injecting a replacement solvent during stirring and filtering so as to ensure that the concentration of the multidimensional nanomaterial in the stirring centrifugal filter cylinder is relatively stable during filtering, and the filtrate outflow collection system is responsible for collecting filtered byproducts.
The method for purifying multi-dimensional nanomaterials by the device for purifying multi-dimensional nanomaterials comprises the following steps:
s1, diluting the nano material mother liquor by a diluent, and injecting the diluted nano material mother liquor into a filter cylinder through a solution injection system;
s2, starting stirring at a fixed stirring speed, and enabling the leaching solvent to continuously flow in through the solution injection system during stirring so as to compensate the loss of the filter liquor flowing away;
s3, stirring for 60-180min, stopping adding the leaching solvent, and continuing to stir the concentrated solution;
s4 when the concentration of the concentrated solution reaches 1mg m L-1-15mg mL-1After that, the purified concentrate was collected at the bottom of the filtration cylinder.
The nanowire mother liquor contains synthesis byproducts such as nano short rods, a surfactant, a surface coating agent, unreacted reactants and the like, the mother liquor solvent is determined according to a method for synthesizing the nano material, and the diluting solvent comprises water, isopropanol, ethanol, ethyl acetate, petroleum ether and the like.
Preferably, the diluent is selected from water, isopropanol, ethanol, ethyl acetate, petroleum ether.
Preferably, the leaching solvent is selected from: selected from water, isopropanol, ethanol, ethyl acetate, petroleum ether.
Preferably, the fixed stirring speed is 80rpm to 1000 rpm.
The beneficial effects of the invention at least comprise:
(1) the invention discloses a method for purifying a nano material based on dynamic stirring centrifugation, which has the advantages of simple steps, mild conditions, high efficiency and high speed, and can be applied to the purification of nano wires and nano sheets.
(2) Compared with the traditional filtration and purification method, the set of dynamic stirring centrifugal filter device has many advantages: firstly, accurately regulating and controlling the filtering pressure based on stirring, wherein the filtering pressure is derived from a centrifugal force generated when liquid is stirred, the filtering pressure is controlled by the stirring rotating speed, the filtering pressure is high when the rotating speed is high, the filtering speed is relatively accelerated, and the filtering speed is low when the rotating speed is not high; the filter membrane is fixed on the filter cylinder through a framework on the filter cylinder, is vertical to the filter base, and has a larger filter area compared with the traditional bottom filtration; thirdly, the shearing force generated by stirring can clean the surface of the filter membrane, so that the nano by-products are prevented from being accumulated and blocking filter holes of the filter membrane, the subsequent filtration efficiency and the continuous filtration capacity are reduced, meanwhile, the repeated utilization of the filter membrane is realized, and the cost is reduced; fourthly, the solvent can be replaced by various target solvents after the nano material is concentrated through a solution injection system, for example, the undesirable high boiling point solvent is replaced; fifthly, the purification, concentration and solvent phase change of the nano material can be realized in one step in stirring, and the post-treatment process is simplified.
Drawings
Fig. 1 is a schematic structural diagram of an apparatus for purifying multi-dimensional nanomaterials according to an embodiment of the invention.
Detailed Description
The technical solutions in the embodiments of the present invention are clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the scope of the present invention.
Example 1
The utility model provides a device of purification multidimension nano-material, includes filter vat, agitating unit, solution injection system, filtrating outflow collecting system, the filter vat comprises filtration base, filtration skeleton and the filter membrane of attached to on filtering the skeleton, the filter membrane passes through the filtration skeleton to be fixed on filtering the base, and is perpendicular with filtering the base.
The method for purifying the multidimensional nano material of the multidimensional nano material purifying device comprises the following steps:
s1, diluting the nano material mother liquor by a diluent, and injecting the diluted nano material mother liquor into a filter cylinder through a solution injection system;
s2, starting stirring, and continuously allowing the leaching solvent to flow in through the solution injection system during stirring to compensate for loss of the filter liquor;
s3, stopping adding the leaching solvent, and continuing to stir the concentrated solution;
s4, collecting the purified concentrated solution at the bottom of the filter cylinder.
Example 2
Diluting 6L silver nanowire mother liquor with ethanol, pouring the diluted solution into a filter cylinder provided with a filter membrane, wherein the aperture of the filter hole of the used filter membrane is 8 mu m, the stirring speed is set to 200rpm, a ten-hole stirring paddle stirs the mixed solution, supplementing solvent water continuously flows into a filter device from an upper solution injection system in the stirring process, the inflow rate is basically the same as the outflow rate of the filter solution, so that the concentration of the stirred filter solution in the filter cylinder is kept relatively stable, the function of replacing the solvent is realized, the silver nanowire dispersion solution solvent is replaced by ethylene glycol with high boiling point and high viscosity into a common solvent, and the stirring and purifying time is that80 minutes later, the addition of the leaching solvent was stopped, and the solution was concentrated to 8mg m L with continued stirring-1. And collecting the purified silver nanowire concentrated solution from the bottom of the filter cylinder.
Example 3
Diluting 6L copper nano-sheet mother liquor with ethyl acetate, pouring the diluted solution into a filtering cylinder provided with a filtering membrane, wherein the aperture of a filtering hole of the used filtering membrane is 4 mu m, the stirring speed is set to 600rpm, a six-hole stirring paddle is used for stirring the mixed solution, a supplementary solvent isopropanol continuously flows into a filtering device from an upper solution injection system in the stirring process, the inflow rate is basically the same as the outflow rate of the filtering liquid, so that the concentration of the stirred filtering liquid in the filtering cylinder is kept relatively stable, the function of replacing the solvent is achieved, the copper nano-sheet dispersion liquid solvent is replaced by common solvent from high-boiling-point high-viscosity glycerol, the stirring purification time is 100 minutes, then, the adding of a leaching solvent is stopped, the stirring is continued, and the solution is-1. And collecting the purified copper nanosheet concentrated solution from the bottom of the stirring centrifugal filter cylinder.
Example 4
Diluting 6L silver nanosheet mother liquor with petroleum ether, pouring into a stirring centrifugal filter cylinder provided with a filter membrane, wherein the aperture of a filter hole of the used filter membrane is 1 mu m, the stirring speed is set to 1000rpm, a ten-hole stirring paddle is used for stirring the mixed liquor, a supplementary solvent ethanol continuously flows into a filter device from an upper solution injection system in the stirring process, the inflow rate is basically the same as the outflow rate of the filtrate, so that the concentration of the stirred filtrate in the filter cylinder is kept relatively stable, the solvent replacement function is achieved, the silver nanosheet dispersion solvent is replaced by high-boiling point high-viscosity ethylene glycol, the stirring purification time is 80 minutes, then the adding of a leaching solvent is stopped, the stirring is continued, and the solution is concentrated to 5mg m L-1. And collecting the purified silver nanosheet concentrated solution from the bottom of the filtering cylinder.
Finally, it is noted that the above-mentioned preferred embodiments illustrate rather than limit the invention, and that, although the invention has been described in detail with reference to the above-mentioned preferred embodiments, it will be understood by those skilled in the art that various changes in form and detail may be made therein without departing from the scope of the invention as defined by the appended claims.
Claims (10)
1. The utility model provides a device of purification multidimension nano-material, its characterized in that includes filter tank, agitating unit, solution injection system, filtrating outflow collecting system, filter tank comprises filtration base, filtration skeleton and the filter membrane of attached to on filtering the skeleton, the filter membrane passes through the filtration skeleton to be fixed on filtering the base, and is perpendicular with filtering the base.
2. The apparatus for purifying multidimensional nanomaterial of claim 1, wherein the size of the filtration pores of the filter membrane is 100nm to 10 μm.
3. The apparatus for purifying multidimensional nanomaterials of claim 1 wherein the agitation device comprises an electric motor and an agitator paddle connected to the electric motor.
4. The apparatus for purifying multidimensional nano materials of claim 3, wherein the stirring paddle is selected from one of a single screw propeller, a double screw propeller, and a perforated stirring paddle.
5. The apparatus for purifying multidimensional nano materials as recited in claim 3, wherein the electric motor is connected to the stirring paddle to stir and generate a centrifugal force during the purification, providing a filtering pressure for the nano materials to filter out by-products on the filtering membrane.
6. The apparatus for purifying multidimensional nano material as recited in claim 1, wherein the solution injection system injects the displacing solvent during the agitation filtration to ensure that the concentration of the multidimensional nano material in the agitation centrifugal filtration cylinder is relatively stable during the filtration, and the filtrate flows out of the collection system to collect the filtered by-products.
7. A method for purifying multi-dimensional nanomaterial using the apparatus for purifying multi-dimensional nanomaterial of any one of claims 1 to 6, comprising the steps of:
s1, diluting the nano material mother liquor by using a diluent, and injecting the diluted nano material mother liquor into a filter vat through a solution injection system;
s2, starting stirring at a fixed stirring speed; while stirring, the leaching solvent continuously flows in through the solution injection system to compensate the loss of the filter liquor flowing away;
s3, stirring for 60-180min, stopping adding the leaching solvent, and continuing to stir the concentrated solution;
s4 when the concentration of the concentrated solution reaches 1mg m L-1-15mg mL-1After that, the purified concentrate was collected at the bottom of the filtration cylinder.
8. The method for purifying multidimensional nano materials as recited in claim 7, wherein the diluent is one or more selected from the group consisting of water, isopropanol, ethanol, ethyl acetate, and petroleum ether.
9. The method of purifying multi-dimensional nanomaterials of claim 7, wherein the eluting solvent is selected from the group consisting of: one or more of water, isopropanol, ethanol, ethyl acetate and petroleum ether.
10. The method of purifying multi-dimensional nanomaterials of claim 7, wherein the fixed stirring speed is 80rpm to 1000 rpm.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202010153071.0A CN111408176B (en) | 2020-03-06 | 2020-03-06 | Method and device for purifying multidimensional nano material |
| PCT/CN2020/117147 WO2021174809A1 (en) | 2020-03-06 | 2020-09-23 | Method and device for purifying multi-dimensional nanomaterial |
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| CN202010153071.0A CN111408176B (en) | 2020-03-06 | 2020-03-06 | Method and device for purifying multidimensional nano material |
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| CN111408176B CN111408176B (en) | 2021-08-17 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112808005A (en) * | 2021-01-07 | 2021-05-18 | 南开大学 | Method for purifying silver nanowire mother liquor by stirring induced centrifugal force-vertical filtration and special device |
| WO2021174809A1 (en) * | 2020-03-06 | 2021-09-10 | 深圳第三代半导体研究院 | Method and device for purifying multi-dimensional nanomaterial |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN114618414B (en) * | 2022-04-22 | 2023-11-07 | 南京康德祥医药科技有限公司 | Reaction kettle for purifying cyclohexenecarboxylic acid and purification method thereof |
| CN115740434B (en) * | 2022-10-10 | 2024-08-30 | 东莞理工学院 | Silver nanowire and separation and purification method thereof |
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| CN111408176B (en) | 2021-08-17 |
| WO2021174809A1 (en) | 2021-09-10 |
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